Osmotic distillation process

• US 6,299,777 B1
• Filed: 08/17/1999
• Issued: 10/09/2001
• Est. Priority Date: 08/17/1999
• Status: Expired due to Term

• Current Assignee: Cms Technologies Holdings, Inc.
• Original Assignee: Cms Technologies Holdings, Inc.
• Inventors: Bowser, John J.
• Primary Examiner(s): FORTUNA, ANA M
• Application Number:
  US09/375,898
• Time in Patent Office: 784 Days
• Field of Search: 210/640, 210/644, 210/645, 210/649, 210/634, 426/425, 426/239, 95/45, 95/52, 95/54, 95/50, 96/6, 435/2, 435/325
• US Class Current: 210/640
• CPC Class Codes: B01D 61/24 Dialysis ; Membrane extraction
• CPC Class Codes: B01D 61/364 Membrane distillation
• CPC Class Codes: B01D 61/365 Osmotic distillation or osmotic evaporation

Abstract

A method of raising the concentration of a liquid mixture utilizes osmotic distillation to transfer a volatile component from the mixture in contact with one side of a nonporous, preferably high free volumes, gas permeable membrane to a strip solution in contact with the other side of the membrane. Due to its nonporous nature the gas permeable membrane resists penetration and wetting by oily components that may be present in the feed mixture. Similarly, occlusion of the membrane by solids to resisted. Preferably, an amorphous copolymer of perfluoro-2,2-dimethyl-1,3-dioxole is useful for the gas permeable membrane. Osmotic distillation utilizing such high free volume, nonporous gas permeable membranes can concentrate difficult liquid mixtures such as pulpy fruit juices and especially, limonene-containing juices, for example, orange juice. The process can be operated at high flux for long durations between membrane cleanings. Additionally, less contamination of the strip solution into the feed mixture occurs to provide a high quality concentrate.

Claims

1. A process for concentrating a liquid feed mixture comprising the steps of

providing a feed m mixture of components present in initial concentration, the mixture comprising a volatile component in which mixture said volatile component is soluble and over which mixture said volatile component has a first vapor pressure, and a strip solution over which the volatile component has a second vapor pressure different from the first vapor pressure;

providing a two sided membrane structure comprising a nonporous membrane on one side and conextensive with a microporous substrate on the second side, the nonporous membrane comprising a polymer composition having a free volume of at least one about 15% and being of a composition which is permeable to the volatile component and not wettable by either the feed mixture or the strip solution;

contacting the feed mixture with the nonporous membrane while contacting the strip solution with the microporous substrate;

maintaining the second vapor pressure below the first vapor pressure, thereby causing the volatile component to permeate the membrane from the feed mixture to the strip solution and thus producing a concentrated liquid mixture comprising components other than the volatile component present at concentration greater than the initial concentration; and

removing the concentrated liquid mixture

in which the feed mixture comprises a temperature sensitive fruit juice selected from the group consisting of orange juice, grape juice, pineapple juice, apple juice, pear juice, cranberry juice and mixtures thereof.

2. The process of claim 1 in which the fruit juice is orange juice.

3. A process for concentrating a liquid feed mixture comprising the steps of

providing a feed mixture of components present in initial concentration, the mixture comprising a volatile component in which mixture said volatile component is soluble and over which mixture said volatile component has a first vapor pressure, and a strip solution over which the volatile component has a second vapor pressure different from the first vapor pressure;

providing a two sided membrane structure comprising a nonporous membrane on one side and coextensive with a microporous substrate on the second side, the nonporous membrane comprising a polymer composition having a free volume of at least about 15% and being of a composition which is permeable to the volatile component and not wettable by either the feed mixture or the strip solution;

contacting the feed mixture with the nonporous membrane while contacting the strip solution with the microporous substrate;

maintaining the second vapor pressure below the first vapor pressure, thereby causing the volatile component to permeate the membrane from the feed mixture to the strip solution and thus producing a concentrated liquid mixture comprising components other than the volatile component present at concentration greater than the initial concentration; and

removing the concentrated liquid mixture,

in which the feed mixture comprises coffee.

4. A process for concentrating a liquid feed mixture comprising the steps of

providing a feed mixture of components present in initial concentration,, the mixture comprising a volatile component in which mixture said volatile component is soluble and over which mixture said volatile component has a first vapor pressure, and a strip solution over which the volatile component has a second vapor pressure different from the first vapor pressure;

providing a two sided membrane structure comprising a nonporous membrane on one side and coextensive with a microporous substrate on the second side, the nonporous membrane comprising a polymer composition having a free volume of at least about 15% and being of a composition which is permeable to the volatile component and not wettable by either the feed mixture or the strip solution;

contacting the feed mixture with the nonporous membrane while contacting the strip solution with the microporous substrate;

maintaining the second vapor pressure below the first vapor pressure, thereby causing the volatile component to permeate the membrane from the feed mixture to the strip solution and thus producing a concentrated liquid mixture comprising components other than the volatile component present at concentration greater than the initial concentration; and

removing the concentrated liquid mixture,

in which the strip solution comprises a component selected from the group consisting of alkaline halide salt, alkaline earth metal halide salt, alkali hydroxide, and mixture thereof.

5. The process of claim 4 in which the salt is selected from the group consisting of sodium chloride, calcium chloride, magnesium chloride, monopotassium phosphate, dipotassium orthophosphate, magnesium sulfate, lithium chloride, lithium bromide, lithium iodide, potassium iodide, sodium iodide and mixture thereof.